US10711212B2 - Procedure and equipment for the production of solid fuel from wastewater sludge - Google Patents

Procedure and equipment for the production of solid fuel from wastewater sludge Download PDF

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US10711212B2
US10711212B2 US14/236,653 US201214236653A US10711212B2 US 10711212 B2 US10711212 B2 US 10711212B2 US 201214236653 A US201214236653 A US 201214236653A US 10711212 B2 US10711212 B2 US 10711212B2
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wastewater sludge
process according
furnace
dryer
equipment
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US20140360093A1 (en
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Istvan Vereckey
ifj. Istvan Vereckey
Bela Bognar
Laszlo Ercsey
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    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L5/00—Solid fuels
    • C10L5/40—Solid fuels essentially based on materials of non-mineral origin
    • C10L5/48—Solid fuels essentially based on materials of non-mineral origin on industrial residues and waste materials
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00—Treatment of sludge; Devices therefor
    • C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/13—Treatment of sludge; Devices therefor by de-watering, drying or thickening by heating
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00—Treatment of sludge; Devices therefor
    • C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00—Treatment of sludge; Devices therefor
    • C02F11/18—Treatment of sludge; Devices therefor by thermal conditioning
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L5/00—Solid fuels
    • C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
    • C10L5/06—Methods of shaping, e.g. pelletizing or briquetting
    • C10L5/08—Methods of shaping, e.g. pelletizing or briquetting without the aid of extraneous binders
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L5/00—Solid fuels
    • C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
    • C10L5/26—After-treatment of the shaped fuels, e.g. briquettes
    • C10L5/28—Heating the shaped fuels, e.g. briquettes; Coking the binders
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L5/00—Solid fuels
    • C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
    • C10L5/34—Other details of the shaped fuels, e.g. briquettes
    • C10L5/36—Shape
    • C10L5/363—Pellets or granulates
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L5/00—Solid fuels
    • C10L5/40—Solid fuels essentially based on materials of non-mineral origin
    • C10L5/46—Solid fuels essentially based on materials of non-mineral origin on sewage, house, or town refuse
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00—Treatment of sludge; Devices therefor
    • C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
    • C02F11/122—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using filter presses
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00—Treatment of sludge; Devices therefor
    • C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
    • C02F11/127—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering by centrifugation
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/10—Biofuels, e.g. bio-diesel
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel

Definitions

  • the subject of the invention relates to a procedure and equipment for the production of solid fuel from wastewater sludge with which solution favourably pellets or briquettes that can be usefully used as fuel are created from material that contaminates the environment.
  • the European Union prescribes the drainage and treatment of communal wastewaters as a compulsory task for settlements with a population over 2000 for the Member States and the National Wastewater Drainage and Treatment Realisation programme was drawn up so that we can comply with this obligation.
  • Hungary would have to triple its number of wastewater treatment plants in a short period of time which would involve a two-and-a-halftimes increase of treatment capacity.
  • the amount of wastewater sludge will also increase many times.
  • With the development of the wastewater network the amount of wastewater sludge created in the wastewater treatment plants will increase at a fast pace.
  • the amount of wastewater sludge created in Hungary is 160-170,000 tonnes of dry material, and this amount may even double by 2015. Counting with a dry material content of 18-25% the annually created wastewater sludge amount approaches 1 million tonnes. Today this is one of the most significant environmental problems in Hungary that still needs to be solved. Among the possible treatment methods depositing is used in a large proportion as a neutralisation solution. It is essential to reduce this amount, as since 1 Jun. 2005 it has been forbidden to deposit wastewater sludge without treatment according to Ministry of Environment decree no 22/2001. (X.IO.) KoM. Use in agriculture is also prominent, but the tightening regulations may reduce this amount to a large extent. A solution to this problem may be utilisation as (alternative) fuel to replace fossil fuels both on the Hungarian and international level.
  • wastewater sludge represents a serious problem in wastewater treatment plants, its environmentally friendly use has not been solved.
  • the primary aim set for the invention is to transform wastewater sludge into a useful material the further utilisation of which is environmentally friendly and clearly advantageous for society.
  • a further objective of the invention is to create a solution through which not only is the problem of individual wastewater treatment plants solved but that also ensures a general solution.
  • pellets are small, with a diameter of a few centimetres at the most, cylindrical-high energy content, products which are pressed using a suitable technology process from appropriately prepared raw material (traditionally wood waste) and which are an excellent natural source of energy and so an economic fuel.
  • the advantages of utilisation as pellets are obvious as an environmentally friendly product is produced from environmentally damaging wastewater sludge, which also has a low hazardous material content and has a high heat content so it can be directly used as fuel, even in the same combustion equipment that is used to produce the pellet.
  • a further advantage of it is that while using it as a fuel the combustion equipment simply atomises it.
  • fuel larger than pellets can also be produced, this process creates briquettes.
  • we produce solid fuel from wastewater sludge which procedure is frequently called pelletizing, irrespective of the size of the solid fuel produced the solid fuel is called pellet.
  • the first principle can be realised using mechanical methods (pressing, centrifuging, suction, filtering) or by bringing the wet material into direct content with materials the water transfer feature of which is much lower.
  • the second principle is related to the heat required for the phase transformation to water vapour.
  • the water binding energy influences the various dehydration principles and drying methods used. If the state of the water is not changed only that water may be removed that is weakly bound to the material.
  • suction vacuum suction
  • the dehydration method is determined partially by the degree of preparation of the material to be dried and partially by the mechanical sensitivity of the material (e.g. fragile material cannot be centrifuged, etc.).
  • a drying technology also exists in the chemical industry. Drying is a complex process, which is preceded by an experimental procedure to determine the composition of the material and how it behaves during drying. We have performed numerous experiments on wastewater sludge, as a result of which we succeeded in finding the solution according to the invention.
  • the air used for the burning is usually pumped in from the external environment, as it can be seen in specification number JP63290316.
  • Air pre-heating is used in industrial boilers, but the pre-heated air is obtained from the post-heating surfaces of the boiler making use of the heat of the relatively lower temperature flue gas.
  • Such a procedure and equipment is presented, for example, by Hungarian patent specification number P0300545.
  • the flow of oxygen and the temperature is regulated, the latter is performed in such a way that a regulated amount of re circulated flue gas is mixed with the incoming fresh air.
  • a further problem is achieving favourable flue gas emission values, which can only be solved by separately inputting other compounds or with an expensive separator built into the flue gas flow.
  • the subject of the invention relates to the production of solid fuel from wastewater sludge, during which the wastewater sludge containing 2-8% dry material is first subjected to mechanical water removal, during which the absorption water is removed and we produce wastewater sludge with a dry material content of at least 25-30%.
  • the significant proportion of the remaining capillary water, favourably at least half of it, is removed by an accelerated evaporation process, drying.
  • the essence of the procedure is that we pre-dry the wastewater sludge containing at least 25-30% dry material using the heat of the flue gas of the burning equipment operated by us to a dry material content of 50-55%, we extract the steam created and gases released during pre-drying, filtering them if necessary and utilise them by returning them to the burning equipment.
  • the subject of the invention also relates to equipment for the production of solid fuel from wastewater sludge, which is connected to a mechanical dehydration unit for the feeding of the wastewater sludge.
  • the output of this is connected to a final dryer through a pre-dryer and pelletizer extruder; furthermore it contains burning equipment connected to the pre-dryer and final dryer.
  • the equipment is set up in such a way that the pre-dryer is a double-walled drum, and there is a spiral-shaped mixing blade fixed inside this drum.
  • the final dryer is fitted with stainless steel bands, and the flue gas output of the burning equipment runs between the steel bands via a heat exchanger.
  • the forced-flow air extraction of the final dryer is connected to the input between the two walls of the double-walled drum of the pre-dryer.
  • the suction connector of the drum is connected with the combustion chamber of the burning equipment, favourably through a filter; furthermore, the output of the final dryer at the end of the steel bands is connected to the burning equipment through the fuel feeder.
  • the outside wall of the burning equipment is fitted with heat insulation and a space(s) that raises the temperature of the gases feeding combustion is(are) formed in the wall and which is(are) connected to the combustion chamber.
  • the equipment has a cooler unit connected to the final dryer and also includes a packaging unit.
  • the equipment is placed in a container(s).
  • This solution is especially practical as with this mobile form of the equipment wastewater treatment plants that are distant from one another can be visited one after the other. It is practical to visit the individual wastewater treatment plants with our mobile equipment according to an appropriate plan, in a given chronological order and when there is a sufficient amount of wastewater sludge available for processing.
  • FIG. 1 shows a block outline of an advantageous construction of the equipment
  • FIG. 2 shows an outline drawing of a practical solution of the pre-dryer.
  • the equipment shown in FIG. 1 is for the production of solid fuel from wastewater sludge, which is connected to a mechanical dehydration unit 2 for the input of wastewater sludge 1 .
  • the output of this is connected to a final dryer 5 via a pre-dryer 3 and pelletizer extruder 4 .
  • it contains burning equipment 6 connected to the pre-dryer 3 and the final dryer 5 .
  • the equipment is set up in such a way that the pre-dryer 3 is a double-walled drum 30 —see FIG. 2 —and there is a spiral mixing blade 31 fixed inside this drum 30 .
  • the final dryer 5 is fitted with stainless steel bands, and the flue gas 61 output 62 of the burning equipment 6 runs between the steel bands via a heat exchanger. It has a cooler unit 7 connected to the final dryer 5 and also includes a packaging unit 8 . In a very practical way the equipment according to the invention is placed in container(s) 10 .
  • FIG. 2 illustrates a practical solution of the pre-dryer 3 , where the forced-flow air extraction 50 of the final dryer 5 is connected to the input 34 between the two walls 32 , 33 of the double-walled drum 30 of the pre-dryer 3 .
  • the suction connector 35 of the drum 30 is connected with the combustion chamber 63 of the burning equipment 3 , favourably through a filter 64 .
  • the output 51 of the final dryer 5 at the end of the steel bands is connected to the burning equipment 6 through the fuel feeder 65 .
  • the outside wall of the burning equipment 6 is fitted with heat insulation and a space(s) that raises the temperature of the gases feeding combustion is(are) formed in the wall and which is(are) connected to the combustion chamber 63 of the burning equipment 6 .
  • the equipment according to the invention operates in detail according to the following.
  • a mechanical dehydration unit 2 is connected for the inputting of the wastewater sludge 1 , during which the absorption water is removed and we produce wastewater sludge with a dry material content of at least 25-30%.
  • the mechanical dehydration unit 2 is known in itself and favourably uses a vacuum or belt press technique.
  • the significant proportion of the remaining capillary water, favourably at least half of it, is removed from the wastewater sludge by an accelerated evaporation process, drying.
  • the solution according to the invention has numerous advantages. As a result of the high combustion temperature continuously maintained in the burning equipment 6 the burning of low calorific value fuel can be realised in a more perfect way, due to this there are lower emissions and a smaller amount of ash is created.
  • the subject of the invention relates to the production of solid fuel from wastewater sludge, during which the wastewater sludge containing 2-8% dry material is first subjected to mechanical water removal, during which the absorption water is removed and we produce wastewater sludge with a dry material content of at least 25-30%.
  • the significant proportion of the remaining capillary water, favourably at least half of it, is removed by an accelerated evaporation process, drying.
  • the essence of the procedure is that we pre-dry the wastewater sludge containing at least 25-30% dry material using the heat of the flue gas of the burning equipment operated by us to a dry material content of 50-55%, we extract the steam created and gases released during pre-drying, filtering them if necessary and utilise them by returning them to the burning equipment.
  • a further subject of the invention relates to equipment for the production of solid fuel from wastewater sludge, which is connected to a mechanical dehydration unit ( 2 ) for the feeding of the wastewater sludge ( 1 ).
  • the output of this is connected to a final dryer ( 5 ) through a pre-dryer ( 3 ) and pelletizer extruder ( 4 ). Furthermore it contains burning equipment ( 6 ) connected to the pre-dryer ( 3 ) and final dryer ( 5 ).
  • the equipment is set up in such a way that the pre-dryer ( 3 ) is a double-walled drum, and there is a spiral-shaped mixing blade fixed inside this drum.
  • the final dryer ( 5 ) is fitted with stainless steel bands, and the flue gas output ( 61 ) of the burning equipment ( 6 ) runs between the steel bands via a heat exchanger ( 62 ).
  • the forced-flow air extraction ( 50 ) of the final dryer ( 5 ) is connected to the input ( 34 ) between the two walls of the double-walled drum of the pre-dryer ( 3 ), the suction connector ( 35 ) of the drum is connected with the combustion chamber of the burning equipment ( 6 ), favourably through a filter ( 64 ). Furthermore, the output ( 51 ) of the final dryer ( 5 ) at the end of the steel bands is connected to the burning equipment ( 6 ) through the fuel feeder ( 65 ).

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Geology (AREA)
  • Water Supply & Treatment (AREA)
  • Hydrology & Water Resources (AREA)
  • Mechanical Engineering (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Treatment Of Sludge (AREA)
  • Drying Of Solid Materials (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
US14/236,653 2011-08-01 2012-07-31 Procedure and equipment for the production of solid fuel from wastewater sludge Active 2035-01-17 US10711212B2 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
HUP1100410 2011-08-01
HU1100410A HUP1100410A2 (en) 2011-08-01 2011-08-01 Process and installation for preparation of solid combustible made of waste water suludge
HU1100410 2011-08-01
PCT/HU2012/000067 WO2013024309A2 (en) 2011-08-01 2012-07-31 Procedure and equipment for the production of solid fuel from wastewater sludge

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US20140360093A1 US20140360093A1 (en) 2014-12-11
US10711212B2 true US10711212B2 (en) 2020-07-14

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US (1) US10711212B2 (ru)
EP (1) EP2739711B1 (ru)
CA (1) CA2880377C (ru)
DK (1) DK2739711T3 (ru)
EA (1) EA026801B1 (ru)
ES (1) ES2659263T3 (ru)
HR (1) HRP20180232T1 (ru)
HU (2) HUP1100410A2 (ru)
LT (1) LT2739711T (ru)
NO (1) NO2739711T3 (ru)
PL (1) PL2739711T3 (ru)
PT (1) PT2739711T (ru)
RS (1) RS56872B1 (ru)
SI (1) SI2739711T1 (ru)
WO (1) WO2013024309A2 (ru)

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ITNA20130033A1 (it) * 2013-06-18 2014-12-19 Giovanni Perillo Trattamento termico dei fanghi biologici civili e industriali per variare lo stato fisico e renderli filtrabili
RU2633762C1 (ru) * 2016-12-13 2017-10-18 Федеральное государственное бюджетное образовательное учреждение высшего образования "Казанский государственный энергетический университет" (ФГБОУ ВО "КГЭУ") Способ получения топливных гранул
CN107500504A (zh) * 2017-10-20 2017-12-22 河南红东方化工股份有限公司 一种高效连续烘干污泥技术
RU2661881C1 (ru) * 2018-04-20 2018-07-20 Сергей Иванович Цыбульский Способ брикетирования угля

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US3529558A (en) * 1968-07-15 1970-09-22 Von Roll Ag Process and mechanical equipment for the concomitant incineration of solid refuse and aqueous sewage sludge
DE3429055A1 (de) 1984-08-07 1986-02-20 Heiner Dipl.-Ing. 4030 Ratingen Kreyenberg Verfahren zur beseitigung von schlaemmen, insbesondere klaer- und faulschlaemmen
US4768292A (en) 1985-05-22 1988-09-06 Sevar Entsorgungsanlagen Gmbh Method and apparatus for drying sewage sludge
US4852269A (en) * 1986-10-29 1989-08-01 Enviro-Gro Technologies, Inc. Combined sewage and lime slude treatment process
DE3933576C1 (en) * 1989-10-07 1991-02-28 Egon 5060 Bergisch Gladbach De Piski Extruding industrial sludge into pellets - increasing dry material content to over 70 per-cent, expelling water
US5215670A (en) * 1990-02-26 1993-06-01 Bio Gro Systems, Inc. Process of drying and pelletizing sludge in indirect dryer having recycled sweep air
DE19851612A1 (de) 1998-11-10 2000-05-11 Baker Hughes De Gmbh Verfahren und Anlage zur Trocknung und Pelletierung von Schlamm, insbesondere Klärschlamm
US6161305A (en) * 1998-02-26 2000-12-19 Andritz-Patentverwaltungs-Gesellschaft M.B.H. Process and plant for mechanical and thermal dewatering of sludges
EP1209127A1 (en) 2000-11-23 2002-05-29 Baker Hughes (Deutschland) GmbH Method and system for production of storage-stable pellets from clarified sludge

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JPH0652126B2 (ja) 1987-05-21 1994-07-06 松下電器産業株式会社 温風機
HUP9602475A2 (hu) 1996-01-08 1998-03-02 Von Roll Umwelttechnik Ag. Eljárás és berendezés hulladékanyag elégetésére hőenergia kinyerése mellett
NO312260B1 (no) 2000-03-24 2002-04-15 Organic Power As Fremgangsmåte og innretning for konvertering av energi ved forbrenning av fast brennstoff

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1209127B (de) * 1959-11-25 1966-01-20 Consulting Ets Waermeempfindliches Aufzeichnungsmaterial und Verfahren zu seiner Herstellung
US3529558A (en) * 1968-07-15 1970-09-22 Von Roll Ag Process and mechanical equipment for the concomitant incineration of solid refuse and aqueous sewage sludge
DE3429055A1 (de) 1984-08-07 1986-02-20 Heiner Dipl.-Ing. 4030 Ratingen Kreyenberg Verfahren zur beseitigung von schlaemmen, insbesondere klaer- und faulschlaemmen
US4768292A (en) 1985-05-22 1988-09-06 Sevar Entsorgungsanlagen Gmbh Method and apparatus for drying sewage sludge
US4852269A (en) * 1986-10-29 1989-08-01 Enviro-Gro Technologies, Inc. Combined sewage and lime slude treatment process
DE3933576C1 (en) * 1989-10-07 1991-02-28 Egon 5060 Bergisch Gladbach De Piski Extruding industrial sludge into pellets - increasing dry material content to over 70 per-cent, expelling water
US5215670A (en) * 1990-02-26 1993-06-01 Bio Gro Systems, Inc. Process of drying and pelletizing sludge in indirect dryer having recycled sweep air
US6161305A (en) * 1998-02-26 2000-12-19 Andritz-Patentverwaltungs-Gesellschaft M.B.H. Process and plant for mechanical and thermal dewatering of sludges
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EA026801B1 (ru) 2017-05-31
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EA201490403A1 (ru) 2014-09-30
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PT2739711T (pt) 2018-02-26
RS56872B1 (sr) 2018-04-30
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